Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
  • H01B3/00—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
  • H01B3/18—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances
  • H01B3/30—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes
  • H01B3/44—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes vinyl resins; acrylic resins
  • H01B3/441—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes vinyl resins; acrylic resins from alkenes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
  • H01B7/00—Insulated conductors or cables characterised by their form
  • H01B7/17—Protection against damage caused by external factors, e.g. sheaths or armouring
  • H01B7/28—Protection against damage caused by moisture, corrosion, chemical attack or weather
  • H01B7/2813—Protection against damage caused by electrical, chemical or water tree deterioration

Definitions

• Various embodiments of the present invention relate to polymeric coatings for coated conductors.
• Such polymeric coatings comprise a a-olefin block composite and an a-olefin based polymer.
• the polymeric coating at least partially surrounds a conductor.
• Power delivery products e.g., power cables
• accessories e.g., joint, termination, and other solid dielectric components
• Water which is usually present at 100 % relative humidity at typical one-meter burial depths, can penetrate through polymeric layers of such products over time.
• a polymeric coating at least partially surrounding said conductive core, wherein said polymeric coating comprises an ⁇ -olefin based polymer and an ⁇ -olefin block composite.
• FIG. 1 is a chart of dielectric breakdown strength for samples prepared in Example 1, specifically dielectric breakdown performance before and after aging in 0.01 M NaCl
• FIG. 2 is a chart of dielectric breakdown strength for samples prepared in Example 1, specifically dielectric breakdown performance before and after aging in 1.0 M NaCl;
• FIG. 3 is a graph of rheological dissipation factor (G"/G') versus shear rate 1/s for samples prepared in Example 2;
• FIG. 4 is a schematic of a U-tube apparatus employed for wet electrical aging.
• Various embodiments of the present invention concern a coated conductor comprising a conductive core at least partially surrounded by a polymeric coating.
• the polymeric coating comprises an a-olefin based polymer and an a-olefin block composite.
• the block composite comprises diblock copolymers having a "hard” polymer segment and a "soft” copolymer segment, as described below.
• the polymeric coating comprises an ⁇ -olefin based polymer.
• a-olefin based polymer denotes a polymer that comprises a majority weight percent ("wt%") of polymerized ⁇ -olefin monomer, based on the total weight of polymerizable monomers, and optionally may comprise at least one polymerized comonomer.
• Comonomers may be other ⁇ -olefin monomers or non-a-olefin monomers.
• the a-olefin based polymer may include greater than 50, at least 60, at least 70, at least 80, or at least 90 wt units derived from an ⁇ -olefin monomer, based on the total weight of the ⁇ -olefin based polymer.
• the ⁇ -olefin based polymer may be a Ziegler-Natta catalyzed polymer, a metallocene-catalyzed polymer, and/or a constrained geometry catalyst catalyzed polymer. Additionally, the ⁇ -olefin based polymers may be made using gas phase, solution, or slurry polymer manufacturing processes.
• Suitable types of ⁇ -olefin monomers include, but are not limited to, C2-20 (i-e., having 2 to 20 carbon atoms) linear, branched or cyclic a-olefins.
• suitable C2-20 ⁇ -olefins include ethylene, propylene, 1-butene, butadiene, isoprene, 4-methyl-l- pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, and 1- octadecene.
• the ⁇ -olefins also can contain a cyclic structure such as cyclohexane or cyclopentane, resulting in an ⁇ -olefin such as 3-cyclohexyl-l-propene (allyl cyclohexane) and vinyl cyclohexane.
• the ⁇ -olefin based polymer can further comprise halogenated groups, such as chlorine, bromine, and fluorine.
• the ⁇ -olefin based polymer can be an interpolymer of ethylene and one or more comonomers.
• Illustrative interpolymers include ethylene/propylene, ethylene/butene, ethylene/l-hexene, ethylene/1 -octene, ethylene/styrene, ethylene/propylene/ 1 -octene, ethylene/propylene/butene, ethylene/butene/1 -octene, ethylene/propylene/diene monomer (“EPDM”) and ethylene/butene/styrene.
• EPDM ethylene/butene/styrene.
• interpolymers can be random interpolymers.
• the a-olefin based polymer comprises polyethylene homopolymer.
• homopolymer denotes a polymer comprising repeating units derived from a single monomer type, but does not exclude residual amounts of other components used in preparing the homopolymer, such as chain transfer agents.
• the a-olefin based polymer can be a low density polyethylene ("LDPE").
• LDPE low density polyethylene
• the term low density polyethylene denotes an ethylene-based polymer having a density range from 0.910 to 0.930 g/cm 3 , as determined by ASTM D792. Relative to high density polyethylene, LDPE has a high degree of short chain branching and/or a high degree of long chain branching.
• the LDPE can have a peak melting temperature of at least 105 °C, or at least 110 °C, up to 115 °C, or 125°C.
• the LDPE can have a melt index ("I 2 ") from 0.5 g/10 min, or 1.0 g/10 min, or 1.5 g/10 min, or 2.0 g/10 min, up to 10.0 g/10 min, or 8.0 g/10 min, or 6.0 g/10 min, or 5.0 g/10 min, or 3.0 g/10 min, as determined according to ASTM D- 1238 (190 °C / 2.16 kg).
• the LDPE can have a polydispersity index (“PDI”) (i.e., weight average molecular weight / number average molecular weight; "Mw/Mn;” or molecular weight distribution (“MWD”)) in the range of from 1.0 to 30.0, or in the range of from 2.0 to 15.0, as determined by gel permeation chromatography.
• PDI polydispersity index
• Mw/Mn number average molecular weight
• MWD molecular weight distribution
• the LDPE is a linear low density polyethylene.
• the ⁇ -olefin based polymer can be a high density polyethylene.
• high density polyethylene (“HDPE”) denotes an ethylene-based polymer having a density greater than or equal to 0.941 g/cm 3 .
• the HDPE has a density from 0.945 to 0.97 g/cm 3 , as determined according to ASTM D-792.
• the HDPE can have a peak melting temperature of at least 130 °C, or from 132 to 134 °C.
• the HDPE can have an I 2 from 0.1 g/10 min, or 0.2 g/10 min, or 0.3 g/10 min, or 0.4 g/10 min, up to 5.0 g/10 min, or 4.0 g/10 min, or, 3.0 g/10 min or 2.0 g/10 min, or 1.0 g/10 min, or 0.5 g/10 min, as determined according to ASTM D-1238 (190 °C / 2.16 kg). Also, the HDPE can have a PDI in the range of from 1.0 to 30.0, or in the range of from 2.0 to 15.0, as determined by gel permeation chromatography.
• the ⁇ -olefin based polymer can be an ethylene-propylene rubber (“EPR") or ethylene-propylene-diene monomer (“EPDM”) polymer.
• the EPR or EPDM polymer can have a peak melting temperature of at least 130 °C, or alternatively, a peak melting temperature from -40 to 100 °C.
• the EPR or EPDM polymer can have an I 2 from 0.10 g/10 min or 5.0 g/10 min, to 20.0 g/10 min, or 100 g/10 min, as determined according to ASTM D-1238 (190 °C / 2.16 kg).
• the EPR or EPDM polymer can have a PDI in the range of from 1.0 to 30.0, or in the range of from 2.0 to 15.0, as determined by gel permeation chromatography.
• the a-olefin based polymer can be a polypropylene.
• the polypropylene can have a peak melting temperature in the range of 150 to 170 °C.
• the polypropylene can have an I 2 from 0.1.0 g/10 min or 5.0 g/10 min, to 20.0 g/10 min, or 100 g/10 min, as determined according to ASTM D-1238 (190 °C / 2.16 kg).
• the polypropylene polymer can have a PDI in the range of from 1.0 to 30.0, or in the range of from 2.0 to 15.0, as determined by gel permeation chromatography.
• the polymeric coating comprises a block composite.
• block composite refers to polymers comprising a soft copolymer, a hard polymer and a block copolymer having a soft segment and a hard segment, where the hard segment of the block copolymer is the same composition as the hard polymer in the block composite and the soft segment of the block copolymer is the same composition as the soft copolymer of the block composite.
• the block copolymers can be linear or branched. More specifically, when produced in a continuous process, the block composites can have a PDI from 1.7 to 15, from 1.8 to 3.5, from 1.8 to 2.2, or from 1.8 to 2.1.
• the block composites When produced in a batch or semi-batch process, the block composites can have a PDI from 1.0 to 2.9, from 1.3 to 2.5, from 1.4 to 2.0, or from 1.4 to 1.8.
• the block composite can be an ⁇ -olefin block composite.
• the term "a-olefin block composite" refers to block composites prepared solely or substantially solely from two or more ⁇ -olefin types of monomers.
• the ⁇ -olefin block composite can consist of only two a- olefin type monomer units.
• An example of an ⁇ -olefin block composite would be a hard segment and hard polymer comprising only or substantially only propylene monomer residues with a soft segment and soft polymer comprising only or substantially only ethylene and propylene comonomer residues.
• hard segments refer to highly crystalline blocks of polymerized units in which a single monomer is present in an amount greater than 95 mole percent ("mol "), or greater than 98 mol . In other words, the comonomer content in the hard segments is less than 5 mol , or less than 2 mol . In some embodiments, the hard segments comprise all or substantially all propylene units. “Soft” segments, on the other hand, refer to amorphous, substantially amorphous or elastomeric blocks of polymerized units having a comonomer content greater than 10 mol . In some embodiments, the soft segments comprise ethylene/propylene interpolymers.
• polyethylene includes homopolymers of ethylene and copolymers of ethylene and one or more C3-8 a-olefins in which ethylene comprises at least 50 mole percent.
• polyethylene copolymer or "propylene interpolymer” means a copolymer comprising propylene and one or more copolymerizable comonomers, where a plurality of the polymerized monomer units of at least one block or segment in the polymer (the crystalline block) comprises propylene, which can be present in an amount of at least 90 mole percent, at least 95 mole percent, or at least 98 mole percent.
• a polymer made primarily from a different a-olefin, such as 4-methyl-l-pentene would be named similarly.
• the term “crystalline” refers to a polymer or polymer block that possesses a first order transition or crystalline melting point (“Tm”) as determined by differential scanning calorimetry ("DSC”) or equivalent technique.
• Tm first order transition or crystalline melting point
• DSC differential scanning calorimetry
• amorphous refers to a polymer lacking a crystalline melting point.
• isotactic denotes polymer repeat units having at least 70 percent isotactic pentads as determined by 13 C-nulcear magnetic resonance (“NMR”) analysis.
• NMR 13 C-nulcear magnetic resonance
• “Highly isotactic” denotes polymers having at least 90 percent isotactic pentads.
• block copolymer or “segmented copolymer” refers to a polymer comprising two or more chemically distinct regions or segments (referred to as “blocks”) joined in a linear manner, that is, a polymer comprising chemically differentiated units which are joined end-to-end with respect to polymerized ethylenic functionality, rather than in pendent or grafted fashion.
• the blocks differ in the amount or type of comonomer incorporated therein, the density, the amount of crystallinity, the crystallite size attributable to a polymer of such composition, the type or degree of tacticity (isotactic or syndiotactic), regio-regularity or regio-irregularity, the amount of branching, including long chain branching or hyper-branching, the homogeneity, or any other chemical or physical property.
• the block copolymers of the invention are characterized by unique distributions of polymer PDI, block length distribution, and/or block number distribution, due, in a preferred embodiment, to the effect of shuttling agent(s) in combination with the catalyst(s) used in preparing the block composites.
• the block composite employed herein can be prepared by a process comprising contacting an addition polymerizable monomer or mixture of monomers under addition polymerization conditions with a composition comprising at least one addition polymerization catalyst, a cocatalyst and a chain shuttling agent ("CSA"), the process being characterized by formation of at least some of the growing polymer chains under differentiated process conditions in two or more reactors operating under steady state polymerization conditions or in two or more zones of a reactor operating under plug flow polymerization conditions.
• CSA chain shuttling agent
• Suitable monomers for use in preparing the block composites of the present invention include any addition polymerizable monomer, such as any olefin or diolefin monomer, including any a-olefin.
• suitable monomers include straight-chain or branched a- olefins of 2 to 30, or 2 to 20, carbon atoms, such as ethylene, propylene, 1-butene, 1-pentene, 3-methyl-l-butene, 1-hexene, 4-methyl- 1-pentene, 3-methyl- 1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene and 1-eicosene; and di- and poly- olefins, such as butadiene, isoprene, 4-methyl- 1,3-pentadiene, 1,3-pentadiene, 1 ,4-pentadiene, 1,5-he
• ethylene and at least one copolymerizable comonomer, propylene and at least one copolymerizable comonomer having from 4 to 20 carbons, 1- butene and at least one copolymerizable comonomer having 2 or from 5 to 20 carbons, or 4- methyl- 1-pentene and at least one different copolymerizable comonomer having from 4 to 20 carbons can be employed.
• the block composites are prepared using propylene and ethylene monomer.
• Comonomer content in the resulting block composites may be measured using any suitable technique, such as NMR spectroscopy. It is highly desirable that some or all of the polymer blocks comprise amorphous or relatively amorphous polymers such as copolymers of propylene, 1-butene, or 4-methyl- 1-pentene and a comonomer, especially random copolymers of propylene, 1-butene, or 4-methyl- 1-pentene with ethylene, and any remaining polymer blocks (hard segments), if any, predominantly comprise propylene, 1-butene or 4- methyl- 1-pentene in polymerized form. Preferably such hard segments are highly crystalline or stereospecific polypropylene, polybutene or poly-4-methyl- 1-pentene, especially isotactic homopolymers.
• amorphous or relatively amorphous polymers such as copolymers of propylene, 1-butene, or 4-methyl- 1-pentene and a comonomer, especially random copolymers of prop
• the block copolymers of the block composites comprise from 10 to 90 wt hard segments and 90 to 10 wt soft segments.
• the mole percent comonomer may range from 5 to 90 wt%, or from 10 to 60 wt%.
• the comonomer is ethylene, it can be present in an amount from 10 to 75 wt%, or from 30 to 70 wt%.
• propylene constitutes the remainder of the soft segment.
• the block copolymers of the block composites comprise hard segments that are 80 to 100 wt% propylene.
• the hard segments can be greater than 90 wt%, 95 wt%, or 98 wt% propylene.
• the block composites described herein may be differentiated from conventional, random copolymers, physical blends of polymers, and block copolymers prepared via sequential monomer addition.
• the block composites may be differentiated from random copolymers by characteristics such as higher melting temperatures for a comparable amount of comonomer, block composite index, as described below; from a physical blend by characteristics such as block composite index, better tensile strength, improved fracture strength, finer morphology, improved optics, and greater impact strength at lower temperature; from block copolymers prepared by sequential monomer addition by molecular weight distribution, rheology, shear thinning, rheology ratio, and in that there is block polydispersity.
• the block composites have a Block Composite Index ("BCI"), as defined below, that is greater than zero but less than 0.4, or from 0.1 to 0.3. In other embodiments, BCI is greater than 0.4 and up to 1.0. Additionally, the BCI can range from 0.4 to 0.7, from 0.5 to 0.7, or from 0.6 to 0.9. In some embodiments, BCI ranges from 0.3 to 0.9, from 0.3 to 0.8, from 0.3 to 0.7, from 0.3 to 0.6, from 0.3 to 0.5, or from 0.3 to 0.4.
• BCI Block Composite Index
• BCI ranges from 0.4 to 1.0, from 0.5 to 1.0, from 0.6 to 1.0, from 0.7 to 1.0, from 0.8 to 1.0, or from 0.9 to 1.0.
• BCI is herein defined to equal the weight percentage of diblock copolymer divided by 100% (i.e., weight fraction).
• the value of the block composite index can range from 0 to 1, wherein 1 would be equal to 100% inventive diblock and zero would be for a material such as a traditional blend or random copolymer.
• the block composites can have a Tm greater than 100 °C, preferably greater than
• the melt flow rate (“MFR") (230 °C, 2.16 kg) of the block composite can range from 0.1 to 1000 dg/min, from 0.1 to 50 dg/min, from 0.1 to 30 dg/min, or from 1 to 10 dg/min.
• the block composites can have a weight average molecular weight (“Mw”) from 10,000 to 2,500,000, from 35,000 to 1,000,000, from 50,000 to 300,000, or from 50,000 to 200,000 g/mol.
• Suitable processes useful in producing the block composites of the invention may be found, for example, in US Patent Application Publication No. 2008/0269412, published on Oct. 30, 2008.
• Suitable catalysts and catalyst precursors for use in the present invention include metal complexes such as disclosed in WO2005/090426, in particular, those disclosed starting on page 20, line 30 through page 53, line 20.
• Suitable catalysts are also disclosed in U.S. 2006/0199930; U.S. 2007/0167578; U.S. 2008/0311812; U.S. 2011/0082258; U.S. Pat. No. 7,355,089; or WO 2009/012215.
• Suitable co-catalysts are those disclosed in WO2005/090426, in particular, those disclosed on page 54, line 1 to page 60, line 12.
• Suitable chain shuttling agents are those disclosed in WO2005/090426, in particular, those disclosed on page 19, line 21 through page 20 line 12.
• Particularly preferred chain shuttling agents are dialkyl zinc compounds.
• the above-described a-olefin based polymer and block composite can be blended to create polymer coatings (e.g., insulation and/or jackets) for wires and/or cables.
• the ⁇ -olefin based polymer can be present in the blend in an amount of at least 10 wt , at least 20 wt , at least 30 wt , or at least 40 wt , up to 90 wt , 80 wt , 70 wt , or 60 wt , based on the combined weight of the ⁇ -olefin based polymer and the block composite.
• the block composite can be present in the blend in an amount of at least 10 wt , at least 20 wt , at least 30 wt , or at least 40 wt , up to 90 wt , 80 wt , 70 wt , or 60 wt , based on the combined weight of the ⁇ -olefin based polymer and the block composite.
• the blend may contain other additives including, but not limited to, organic peroxides, processing aids, fillers, coupling agents, ultraviolet absorbers or stabilizers, antistatic agents, nucleating agents, slip agents, plasticizers, lubricants, viscosity control agents, tackifiers, anti-blocking agents, surfactants, extender oils, acid scavengers, flame retardants, moisture cure catalysts, vinyl alkoxysilane, and metal deactivators.
• additives including, but not limited to, organic peroxides, processing aids, fillers, coupling agents, ultraviolet absorbers or stabilizers, antistatic agents, nucleating agents, slip agents, plasticizers, lubricants, viscosity control agents, tackifiers, anti-blocking agents, surfactants, extender oils, acid scavengers, flame retardants, moisture cure catalysts, vinyl alkoxysilane, and metal deactivators.
• Additives, other than fillers are typically used in amounts ranging from 0.01 or
• Fillers are generally added in larger amounts although the amount can range from as low as 0.01 or less to 65 or more wt based on the weight of the composition.
• Illustrative examples of fillers include clays, precipitated silica and silicates, fumed silica, calcium carbonate, titanium dioxide, magnesium oxide, metal oxides, ground minerals, aluminum trihydroxide, magnesium hydroxide, and carbon blacks with typical arithmetic mean particle sizes larger than 15 nanometers.
• antioxidants can be employed with the polymeric coating.
• exemplary antioxidants include hindered phenols (e.g., tetrakis [methylene (3,5-di-t-butyl-4- hydroxyhydrocinnamate)] methane); phosphites and phosphonites (e.g., tris (2,4-di-t- butylphenyl) phosphate); thio compounds (e.g., dilaurylthiodipropionate); various siloxanes; and various amines (e.g., polymerized 2,2,4-trimethyl-l,2-dihydroquinoline).
• Antioxidants can be used in amounts of 0.1 to 5 wt based on the total composition weight of the polymeric coating material.
• the polymeric coating comprises no or substantially no water tree retarding additives.
• substantially no shall denote a concentration of less than 10 parts per million (“ppm") based on the entire polymeric coating weight.
• the polymeric coating comprises no or substantially no polyethylene glycol.
• Compounding of the polymeric coating can be effected by standard equipment known to those skilled in the art.
• Examples of compounding equipment are internal batch mixers, such as a BanburyTM or BoilingTM internal mixer.
• continuous single, or twin screw, mixers can be used, such as a FarrelTM continuous mixer, a Werner and PfleidererTM twin screw mixer, or a BussTM kneading continuous extruder.
• the blended polymeric coating can have a wet aged dielectric breakdown of at least 25 kV/mm, at least 30 kV/mm, or at least 35 kV/mm. In various embodiments, the blended polymeric coating can have a wet aged dielectric breakdown in the range of from 25 to 45 kV/mm, in the range of from 30 to 40 kV/mm, or in the range of from 35 to 40 kV/mm. Dielectric breakdown is determined according to ASTM D149-09. Wet aging is performed according to the procedure described in the following examples, determined using 0.01, 1.0, or 3.5 M sodium chloride ("Nad”) aqueous solution for 21 days.
• Nad sodium chloride
• the blended polymeric coating can have a breakdown strength retention of at least 70%, at least 80%, at least 90%, at least 95%, or at least 98%, upon wet aging in 3.5 M NaCl aqueous solution for 21 days, as determined on plaques having a thickness of 40 mils and a 2-inch diameter according to ASTM D 149-09.
• a cable comprising a conductor and an insulation layer can be prepared employing the above-described polymeric coating blend.
• a cable containing an insulation layer comprising the polymeric coating blend can be prepared with various types of extruders (e.g., single or twin screw types).
• extruders e.g., single or twin screw types.
• a description of a conventional extruder can be found in USP 4,857,600.
• the extruded intermediate cable can pass into a heated cure zone downstream of the extrusion die to aid in cross-linking the polymeric coating in the presence of a cross-linking catalyst.
• the heated cure zone can be maintained at a temperature in the range of 175 to 260 °C.
• the heated zone can be heated by pressurized steam or inductively heated by pressurized nitrogen gas.
• Alternating current cables prepared according to the present disclosure can be low voltage, medium voltage, high voltage, or extra-high voltage cables. Further, direct current cables prepared according to the present disclosure include high or extra-high voltage cables.
• Wire means a single strand of conductive metal, e.g., copper or aluminum, or a single strand of optical fiber.
• “Cable” and “power cable” mean at least one wire or optical fiber within a sheath, e.g., an insulation covering or a protective outer jacket.
• a cable is two or more wires or optical fibers bound together, typically in a common insulation covering and/or protective jacket.
• the individual wires or fibers inside the sheath may be bare, covered or insulated.
• Combination cables may contain both electrical wires and optical fibers.
• the cable can be designed for low, medium, and/or high voltage applications. Typical cable designs are illustrated in USP 5,246,783, 6,496,629 and 6,714,707.
• Conductor denotes one or more wire(s) or fiber(s) for conducting heat, light, and/or electricity.
• the conductor may be a single-wire/fiber or a multi-wire/fiber and may be in strand form or in tubular form.
• suitable conductors include metals such as silver, gold, copper, carbon, and aluminum.
• the conductor may also be optical fiber made from either glass or plastic.
• Polymer means a macromolecular compound prepared by reacting (i.e., polymerizing) monomers of the same or different type.
• Polymer includes homopolymers and interpolymers.
• Interpolymer means a polymer prepared by the polymerization of at least two different monomers. This generic term includes copolymers, usually employed to refer to polymers prepared from two different monomers, and polymers prepared from more than two different monomers, e.g., terpolymers (three different monomers), tetrapolymers (four different monomers), etc.
• Density is determined according to ASTM D792, method B, on samples as prepared under ASTM D1928. Density measurements are made within one hour of sample pressing. Melt Index
• Dielectric breakdown strength is determined according to ASTM D149-09.
• the materials employed in the following examples are as follows.
• the low density polyethylene (“LDPE”) is DXM-446, commercially available from The Dow Chemical Company, having a density of 0.92 g/cm 3 , a melting point of 108 °C, and a melt index (I 2 ) of about 2.1.
• the block composite 1 is an isotactic polypropylene/ethylene -propylene composition (“iPP-EP”) (40/60 w/w ethylene-propylene to isotactic polypropylene; 65 wt ethylene in ethylene-propylene block).
• the block composite 2 is an isotactic polypropylene/ethylene-propylene composition ("iPP-EP”) (20/80 w/w ethylene-propylene to isotactic polypropylene; 65 wt ethylene in ethylene-propylene block).
• iPP-EP isotactic polypropylene/ethylene-propylene composition
• Catalyst- 1 ([[rel-2',2"'-[(lR,2R)-l,2-cylcohexanediylbis(methyleneoxy-KO)] bis[3- (9H-carbazol-9-yl)-5-methyl[l,l'-biphenyl]-2-olato- ⁇ 0]](2-)]dimethyl-hafnium) and cocatalyst-1, a mixture of methyldi(Ci4_i 8 alky 1) ammonium salts of tetrakis(pentafluorophenyl)borate, prepared by reaction of a long chain trialkylamine (ArmeenTM M2HT, available from Akzo-Nobel, Inc.), HC1 and Li[B(C 6 F 5 ) 4 ], substantially as disclosed in USP 5,919,983, Ex. 2., are purchased from Boulder Scientific and used without further purification.
• ArmeenTM M2HT available from Akzo-No
• CSA-1 diethylzinc or DEZ
• cocatalyst-2 modified methylalumoxane (“MMAO”)
• the solvent for the polymerization reactions is a hydrocarbon mixture (ISOPAR ® E) obtainable from ExxonMobil Chemical Company and purified through beds of 13-X molecular sieves prior to use.
• the block composites are prepared using two continuous stirred tank reactors ("CSTR") connected in series.
• the first reactor is approximately 12 gallons in volume while the second reactor is approximately 26 gallons.
• Each reactor is hydraulically full and set to operate at steady state conditions.
• Monomers, solvent, hydrogen, catalyst- 1, cocatalyst-1, cocatalyst-2 and CSA-1 are fed to the first reactor according to the process conditions outlined in Table 1.
• the first reactor contents as described in Table 1 flow to a second reactor in series. Additional monomers, solvent, hydrogen, catalyst- 1, cocatalyst-1, and optionally, cocatalyst-2, are added to the second reactor.
• FIGS. 1 and 2 demonstrate that the iPP-EP block composite by itself and its blend with LDPE can improve the wet aging of insulation compounds for power cable applications.
• LDPE control comparative sample 1
• LDPE control 1.0 M NaCl condition
• HFDB-4202 is a tree-retardant cross-linked polyethylene
• Table 5 demonstrates that the iPP-EP block copolymer by itself and its blend with LDPE can improve the dielectric breakdown strength retention after wet aging of insulation compounds for power cable applications, even in the absence of a tree retardant additive and under very high salinity conditions.
• the retention of dielectric breakdown strength of the iPP-EP block copolymer by itself as well as its blends with LDPE is about the same or higher compared to the TR-XLPE, and significantly higher than the LDPE.
• Example 7-10 Viscoelasticity

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